2014
DOI: 10.1016/j.fuel.2014.07.047
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Modeling kinetics-transport interactions during biomass torrefaction: The effects of temperature, particle size, and moisture content

Abstract: ABSTRACT:A comprehensive one-dimensional model accounting for the effects of heat and mass transfer, chemical kinetics, and drying was developed to describe the torrefaction of a single woody biomass particle. The thermochemical sub-models depend only on previously determined or measured characteristics, avoiding the use of fitting or tuning parameters and enabling a rigorous energy balance of the process. Moreover, a high temperature drying sub-model is introduced which overcomes the difficulties associated w… Show more

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Cited by 95 publications
(36 citation statements)
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“…A higher parameter is required to model the lab-reactor experiments due to the higher extent of secondary charring. Moreover, even though slow heating rates have been employed in the lab-scale experiments, intra-particle gradients can be present due to the endothermic drying, heat transfer limitations during the heat-up phase and exothermic reactions afterwards [34]. The ''x" parameter may to some extent include these phenomena.…”
Section: Model Resultsmentioning
confidence: 99%
“…A higher parameter is required to model the lab-reactor experiments due to the higher extent of secondary charring. Moreover, even though slow heating rates have been employed in the lab-scale experiments, intra-particle gradients can be present due to the endothermic drying, heat transfer limitations during the heat-up phase and exothermic reactions afterwards [34]. The ''x" parameter may to some extent include these phenomena.…”
Section: Model Resultsmentioning
confidence: 99%
“…Some of the produced steam travels to colder area where it could condense. It was thought that thermal models and Arrhenius type models would be too simplistic to accurately describe these phenomena [44][45][46][47][48]. Drying was therefore modelled using liquid-vapour equilibrium featuring liquid, bound water and steam transport.…”
Section: Drying Modelmentioning
confidence: 99%
“…As identified in the time‐scale analysis, the dominant heat transfer resistance for millimeter‐scale particles is external. For actively pyrolyzing particles, mass transfer occurs rapidly outward and is driven by the increased internal gas pressure from freshly formed volatile products . As a result, intraparticle reactions are neglected and the particles can be assumed to be internally uniform—heating up according to the following time varying temperature profile, Tbio|t=Tr|TrTbio,0normalexp|t/text,HX where T r is the reactor temperature in K, T bio,0 is the initial temperature of the biomass entering the reactor, and characteristic time‐scale for heat transfer t ext,HX is identical to that shown in Table .…”
Section: Mathematical Modelmentioning
confidence: 99%
“…The cold gas efficiency based on the higher heating value (HHV) of all gas phase components divided by the heating value of the fed biomass, ηHHV=j=1NsHHVjtrueṁj,outHHVbiotrueṁbio where the (HHV) of the biomass is computed from its ultimate analysis while the gas phase component HHV's are computed from their standard enthalpies of formation using a separate routine.…”
Section: Mathematical Modelmentioning
confidence: 99%